Modified Zeolite Catalyst for Propylene Selectivity in MTO Process

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Solution Overview

Problem

Current Methanol to Olefin (MTO) processes lack flexibility to control the Propylene to Ethylene (P/E) product ratio, which is crucial for maximizing propylene production due to its high demand, and involve complex reactor systems that increase project costs.

Innovation Solution

A zeolite catalyst with a layered pentasil structure, modified with silica or fluorine, is used in an oxygenate conversion reactor to enhance propylene selectivity, allowing for longer catalyst residence times and reduced regeneration requirements, and can be employed in both fluidized and fixed bed reactor systems.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Adaptability or versatility

If conventional MTO processes are used, then ethylene and propylene are produced, but the Propylene to Ethylene (P/E) product ratio cannot be controlled and is generally low

Engineering Contradiction:
ImproveP/E product ratio control flexibilityVSAvoidpropylene production
Core Design Contradiction:
Adaptability or versatilityVSProductivity

Solution Approach 1:

The patent modifies the MFI zeolite catalyst by changing its chemical composition parameters (adding gallium, iron, boron, or other elements) and physical structure (creating layered pentasil structure with specific Si/Al ratios). These parameter changes enable the catalyst to selectively promote propylene formation over ethylene, achieving controllable P/E ratios greater than 3 while maintaining high productivity

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent creates composite catalyst materials by combining MFI zeolite with other elements (gallium, iron, boron, or rare earth elements) to form composite catalyst systems. This composite structure allows simultaneous optimization of catalytic activity for propylene production and selectivity control, resolving the contradiction between P/E ratio flexibility and propylene productivity

Inventive Principle:
Principle #40Composite materials

2Productivity

If multiple reactors and separation stages are used to maximize ethylene and propylene, then productivity increases, but device complexity increases

Engineering Contradiction:
Improveolefin productionVSAvoidreactor system complexity
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The modified MFI zeolite catalyst performs multiple functions within a single reactor: it catalyzes the conversion of oxygenates to olefins, selectively promotes propylene formation, and maintains stable activity over extended periods. This multi-functionality eliminates the need for multiple specialized reactors and complex separation systems, reducing device complexity while maintaining high olefin productivity

Inventive Principle:
Principle #6Universality (Multi-functionality)

3Productivity

If standard MFI zeolite catalyst is used, then oxygenate conversion occurs, but catalyst deactivation is rapid requiring frequent regeneration

Engineering Contradiction:
Improveoxygenate conversion rateVSAvoidcatalyst residence time
Core Design Contradiction:
ProductivityVSDuration of action of stationary object

Solution Approach 1:

The patent creates composite catalyst materials by incorporating gallium, iron, boron, or rare earth elements into the MFI zeolite structure. These composite materials maintain high catalytic activity for oxygenate conversion while the added elements stabilize the catalyst structure, preventing rapid deactivation and extending catalyst residence time between regenerations

Inventive Principle:
Principle #40Composite materials

Solution Approach 2:

The patent creates layered pentasil structure with specific local structural characteristics and controls the distribution of metal elements within the zeolite framework. This local structural optimization maintains high activity sites for oxygenate conversion while the overall layered structure provides stability, resolving the contradiction between conversion rate and catalyst durability

Inventive Principle:
Principle #3Local quality

Applied Scientific Principles

This section explains which scientific principles are used to turn an abstract innovation direction into a practical engineering solution.

Function Achieved in This Case

The process achieves high propylene selectivity (47% to 52%) with low ethylene selectivity (3% to 6%), improving the economic viability of propylene production and simplifying the reactor system complexity.

Implementation Method 1

The oxygenate feed stock is catalytically converted to paraffin's, light olefins (ethylene, propylene) and heavier olefins using a silicoaluminophosphate (SAPO) molecular sieve catalyst in the vapor phase

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

the surface of the catalyst has been modified with silica or fluorine

Methodology Applied
Scientific EffectAdsorption: Adsorption

Data Source

PatentUS9643897B2Enhanced propylene production in OTO process with modified zeolites
Publication Date: 2017.05.09 UOP LLC

AI summary

A process for oxygenate conversion using a family of crystalline aluminosilicate zeolites that is a layered pentasil zeolite with a silica or fluorine modified surface. These zeolites are represented by the empirical formula:Mmn+Rrp+Al1-xExSiyOz where M is an alkali, alkaline earth, or rare earth metal such as sodium or potassium, R can be a mixture of organoammonium cations and E is a framework element such as gallium, iron, boron, or indium. These zeolites are characterized by unique x-ray diffraction patterns and compositions and have catalytic properties for carrying out oxygenate conversion processes.